US6814481B2 - Screw extruder with improved mixing pins - Google Patents
Screw extruder with improved mixing pins Download PDFInfo
- Publication number
- US6814481B2 US6814481B2 US10/399,111 US39911103A US6814481B2 US 6814481 B2 US6814481 B2 US 6814481B2 US 39911103 A US39911103 A US 39911103A US 6814481 B2 US6814481 B2 US 6814481B2
- Authority
- US
- United States
- Prior art keywords
- extruder
- pin members
- pairs
- extruder according
- cylindrical chamber
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime, expires
Links
- 238000001125 extrusion Methods 0.000 claims abstract description 23
- 239000000463 material Substances 0.000 claims abstract description 14
- 239000012530 fluid Substances 0.000 claims description 5
- 230000000694 effects Effects 0.000 claims description 3
- 230000001105 regulatory effect Effects 0.000 claims description 3
- 229920001971 elastomer Polymers 0.000 abstract description 3
- 239000000806 elastomer Substances 0.000 abstract description 2
- 239000012634 fragment Substances 0.000 description 2
- 239000011324 bead Substances 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 239000012809 cooling fluid Substances 0.000 description 1
- 238000003780 insertion Methods 0.000 description 1
- 230000037431 insertion Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/78—Thermal treatment of the extrusion moulding material or of preformed parts or layers, e.g. by heating or cooling
- B29C48/80—Thermal treatment of the extrusion moulding material or of preformed parts or layers, e.g. by heating or cooling at the plasticising zone, e.g. by heating cylinders
- B29C48/83—Heating or cooling the cylinders
- B29C48/834—Cooling
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/395—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/50—Details of extruders
- B29C48/68—Barrels or cylinders
- B29C48/685—Barrels or cylinders characterised by their inner surfaces, e.g. having grooves, projections or threads
- B29C48/687—Barrels or cylinders characterised by their inner surfaces, e.g. having grooves, projections or threads having projections with a short length in the barrel direction, e.g. pins
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
Definitions
- the present invention relates to an extruder provided with mixing pins.
- screw extruders are generally composed of an extruder body with a cylindrical chamber containing, longitudinally, a helical screw which, when rotated, pushes, mixes and compresses the extrusion material towards an extrusion head on which a die is mounted.
- the cylindrical chamber contains mixing pins or rods.
- the pins are normally arranged at regular intervals in the longitudinal direction and inserted radially in the casing of the extruder body.
- the pins are fit in the casing walls, opposite interruptions in the thread of the extrusion screw, and also project inwardly the cylindrical chamber by a distance which is undoubtedly less than the transverse dimension of the gap between the core of the screw and the internal surface of the said chamber.
- the main functions of the pins is that of creating an obstacle to the feeding movement of the extrusion material, which is thus disturbed and mixed more thoroughly, and of exchanging heat with extrusion material.
- a first problem is linked with the impossibility of correctly regulating the temperature of these pins.
- U.S. Pat. No. 5,324,108 discloses a pin cylinder extruder wherein some pins are provided tangentially in the chamber. Such pins have an internal dead hole where thermal fluid is made to circulate back and fort. Such a kind of circulation path for the thermal fluid is not efficient and requires that the internal diameter of the pins be sufficiently large to accomodate an exit tube.
- the fragments which break off end up inside the cylindrical chamber, contaminating the extrusion material and, in the worst instance, damaging the extrusion screw or the actual cylindrical chamber.
- U.S. Pat. No. 5,480,227 discloses a screw extruder provided with some diagonally inclined pins.
- the wall of the cylinder receiving the screw has an anular recess.
- Pins are located very close to a bead of the screw and partially embedded in said cylinder wall. In this way, the extruded material may come into contact with a small portion of the lateral surface of the pins, resulting in a poor thermal exchange.
- extruded material is chennelled between the pins but not actually mixed.
- the object of the present invention is to overcome the problems encountered in the prior art by providing a new and original design of extruder in which the temperature of the pins can be easily controlled even with small diameters, the extrusion material may be intimately mixed and thermally regulated by the pins and it is possible to prevent damage resulting from possible breakage of these pins.
- FIG. 1A is a longitudinally sectioned view through an extruder body according to the prior art
- FIG. 1B is a cross-sectional view taken along the line I-I of FIG. 1A;
- FIG. 2 is a partial longitudinal section through an extruder body according to the invention.
- FIG. 3 is a cross-sectional view along the line III-II in FIG. 2 .
- An extruder comprises, in a manner known per se, an extruder body 1 containing a cylindrical chamber 2 which longitudinally houses an extrusion screw 3 .
- the extrusion screw 3 is composed of a core N and a thread F which is spirally wound around the core N with a constant or variable pitch depending on the circumstances.
- Rotation of the screw which is obtained by means of known actuating means (not shown), causes feeding and compression of an extrusion material (in particular rubber, elastomer material or the like) introduced into the cylindrical chamber via a suitable loading opening (not shown).
- an extrusion material in particular rubber, elastomer material or the like
- mixing pin members 4 which pass through the whole of the thickness of the facing walls of the extruder body 1 and the cylindrical chamber 2 are provided.
- the pin members 4 are inserted and fixed inside suitable insertion holes in the extruder body so as to be tangential, and very close, to the core N of the extrusion screw 3 .
- Each pin member is composed of a hollow rod 4 a which has, fixed to its ends, locking bushes 4 b (for example engaged with the respective rod by means of a thread) by means of which the pin members are locked tightly on the extruder body.
- the thread F has an interruption Fi.
- the rods are arranged in pairs on either side of the core N. Moreover, the pairs of rods are distributed longitudinally, alternating at 90° with respect to each other (FIG. 2 ).
- the rods 4 a are tubular, namely they have at least one internal flow channel through which a heat-regulating liquid (for example oil or hot water or a cooling fluid, depending on the circumstances) can be circulated.
- a heat-regulating liquid for example oil or hot water or a cooling fluid, depending on the circumstances
- the fluid is circulated by introducing it at one end of the hollow rod 4 a and allowing it flow out at the opposite end by means of suitable delivery and return pipes (not shown).
- the rods according to the invention allow a continuous flow of a heat-regulating fluid, such that it is possible to control in an optimum manner the temperature in accordance with the specific requirements. Moreover, since they are fixed to the extruder body at both ends, even if the portion inside the cylindrical chamber should break, they nevertheless would remain attached to the extruder body without their fragments being able to end up inside the chamber.
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Abstract
An extruder, in particular for elastomer material, is described, said extruder being of the type comprising an extruder body (1) provided with a cylindrical chamber (2) inside which an extrusion screw is rotatably inserted, and a plurality of mixing rods (4) inserted in the casing (1) of the cylindrical chamber (2) and projecting inside the said chamber (2) wherein each rod (4) is arranged tangential to the core of said screw(3) opposite interruptions in the thread of the screw (3) and passes through the whole of the chamber (2) engaging in both the opposite walls of said casing (1). <IMAGE>
Description
The present invention relates to an extruder provided with mixing pins.
As is known, screw extruders are generally composed of an extruder body with a cylindrical chamber containing, longitudinally, a helical screw which, when rotated, pushes, mixes and compresses the extrusion material towards an extrusion head on which a die is mounted.
According to the prior art it is also envisaged, in certain cases, that the cylindrical chamber contains mixing pins or rods. As can be seen from FIGS. 1A and 1B, which show an extrusion cylinder according to the prior art, the pins are normally arranged at regular intervals in the longitudinal direction and inserted radially in the casing of the extruder body.
In order to prevent interference during operation, the pins are fit in the casing walls, opposite interruptions in the thread of the extrusion screw, and also project inwardly the cylindrical chamber by a distance which is undoubtedly less than the transverse dimension of the gap between the core of the screw and the internal surface of the said chamber.
The main functions of the pins is that of creating an obstacle to the feeding movement of the extrusion material, which is thus disturbed and mixed more thoroughly, and of exchanging heat with extrusion material.
However, at least two types of problem are associated with this configuration.
A first problem is linked with the impossibility of correctly regulating the temperature of these pins.
U.S. Pat. No. 5,324,108 discloses a pin cylinder extruder wherein some pins are provided tangentially in the chamber. Such pins have an internal dead hole where thermal fluid is made to circulate back and fort. Such a kind of circulation path for the thermal fluid is not efficient and requires that the internal diameter of the pins be sufficiently large to accomodate an exit tube.
Moreover, in the event of one or more of the rods breaking, the fragments which break off end up inside the cylindrical chamber, contaminating the extrusion material and, in the worst instance, damaging the extrusion screw or the actual cylindrical chamber.
U.S. Pat. No. 5,480,227 discloses a screw extruder provided with some diagonally inclined pins. The wall of the cylinder receiving the screw has an anular recess. Pins are located very close to a bead of the screw and partially embedded in said cylinder wall. In this way, the extruded material may come into contact with a small portion of the lateral surface of the pins, resulting in a poor thermal exchange. Moreover, extruded material is chennelled between the pins but not actually mixed.
The object of the present invention is to overcome the problems encountered in the prior art by providing a new and original design of extruder in which the temperature of the pins can be easily controlled even with small diameters, the extrusion material may be intimately mixed and thermally regulated by the pins and it is possible to prevent damage resulting from possible breakage of these pins.
These objects are achieved by means of a screw extruder as described in claim 1.
Further characteristic features and advantages of the device according to the invention will emerge, however, more clearly from the following detailed description provided by way of example and illustrated in the accompanying drawings, in which:
FIG. 1A is a longitudinally sectioned view through an extruder body according to the prior art;
FIG. 1B is a cross-sectional view taken along the line I-I of FIG. 1A;
FIG. 2 is a partial longitudinal section through an extruder body according to the invention; and
FIG. 3 is a cross-sectional view along the line III-II in FIG. 2.
An extruder comprises, in a manner known per se, an extruder body 1 containing a cylindrical chamber 2 which longitudinally houses an extrusion screw 3.
The extrusion screw 3 is composed of a core N and a thread F which is spirally wound around the core N with a constant or variable pitch depending on the circumstances.
Rotation of the screw, which is obtained by means of known actuating means (not shown), causes feeding and compression of an extrusion material (in particular rubber, elastomer material or the like) introduced into the cylindrical chamber via a suitable loading opening (not shown).
According to the invention, mixing pin members 4 which pass through the whole of the thickness of the facing walls of the extruder body 1 and the cylindrical chamber 2 are provided. The pin members 4 are inserted and fixed inside suitable insertion holes in the extruder body so as to be tangential, and very close, to the core N of the extrusion screw 3.
Each pin member is composed of a hollow rod 4 a which has, fixed to its ends, locking bushes 4 b (for example engaged with the respective rod by means of a thread) by means of which the pin members are locked tightly on the extruder body.
At the point where the chamber 2 is passed through by one of the rods 4, the thread F has an interruption Fi.
Preferably, the rods are arranged in pairs on either side of the core N. Moreover, the pairs of rods are distributed longitudinally, alternating at 90° with respect to each other (FIG. 2).
The rods 4 a are tubular, namely they have at least one internal flow channel through which a heat-regulating liquid (for example oil or hot water or a cooling fluid, depending on the circumstances) can be circulated.
As shown schematically in FIG. 3, the fluid is circulated by introducing it at one end of the hollow rod 4 a and allowing it flow out at the opposite end by means of suitable delivery and return pipes (not shown).
Further, as can be well appreciated from FIG. 3, between the rods 4 a and the internal surface of the cylinder wall a substantial clearance 5 is left. In other words, at least a portion of said rods is wholly wetted by the extrusion material. This allows the extrusion material to pass all around the pin members, so as to contact a major portion thereof and enhance the thermal exchange effect. Moreover, the two extrusion material streams, coming from the two sides of the rod 4 a during extrusion, meet each other downstream of the rod 4 a resulting in an enhanced mixing effect.
The rods according to the invention allow a continuous flow of a heat-regulating fluid, such that it is possible to control in an optimum manner the temperature in accordance with the specific requirements. Moreover, since they are fixed to the extruder body at both ends, even if the portion inside the cylindrical chamber should break, they nevertheless would remain attached to the extruder body without their fragments being able to end up inside the chamber.
This latter characteristic feature is of considerable importance and means that major savings may be made with regard to repair and maintenance costs.
It is understood, however, that the scope of protection of the invention described above is not limited to the particular embodiment shown, but that it is extended to any other constructional modification which achieves the same usefulness.
For example, although mixing pin members with a circular cross-section have been described, it is also possible to use, in particular circumstances, tubular rods with a differently profiled cross-section.
Claims (9)
1. Extruder of the type comprising an extruder body with a cylindrical chamber inside which an extrusion screw is rotatably inserted, a plurality of mixing thermally regulated pin members being inserted through ceasing of said cylindrical chamber and being fixed with their respective ends to the wall of said extruder, characterized in that at least a portion of said rods projects inside said cylindrical chamber in such a way that its entire circumferential surface may be wetted by the extrusion material so as to enhance heat exchange and mixing effect.
2. Extruder according to claim 1 , in which said pin members comprise an hollow rod and a heat-regulating fluid is circulated inside them.
3. Extruder according to claim 2 , in which said rods consist of a tubular rod, the ends of which emerge externally from said extruder body and are fixed thereon by means of fixing bushes.
4. Extruder according to claim 3 , in which said pin members are provided in pairs, one on one side and one on the opposite side of the extrusion screw.
5. Extruder according to claim 4 , in which said pairs of pin members are arranged longitudinally, alternating at 90° with respect to each other.
6. Extruder according to claim 2 , in which said pin members are provided in pairs, one on one side and one on the opposite side of the extrusion screw.
7. Extruder according to claim 6 , in which said pairs of pin members are arranged longitudinally, alternating at 90° with respect to each other.
8. Extruder according to claim 1 , in which said pin members are provided in pairs, one on one side and one on the opposite side of the extrusion screw.
9. Extruder according to claim 8 , in which said pairs of pin members are arranged longitudinally, alternating at 90° with respect to each other.
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP01830096.2 | 2001-02-14 | ||
EP01830096A EP1232847A1 (en) | 2001-02-14 | 2001-02-14 | Pin-barrel extruder |
EP01830096 | 2001-02-14 | ||
PCT/EP2002/001417 WO2002068174A1 (en) | 2001-02-14 | 2002-02-11 | Screw extruder with improved mixing pins |
Publications (2)
Publication Number | Publication Date |
---|---|
US20040115297A1 US20040115297A1 (en) | 2004-06-17 |
US6814481B2 true US6814481B2 (en) | 2004-11-09 |
Family
ID=8184399
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US10/399,111 Expired - Lifetime US6814481B2 (en) | 2001-02-14 | 2002-02-11 | Screw extruder with improved mixing pins |
Country Status (6)
Country | Link |
---|---|
US (1) | US6814481B2 (en) |
EP (2) | EP1232847A1 (en) |
AT (1) | ATE296722T1 (en) |
DE (1) | DE60204425T2 (en) |
ES (1) | ES2242847T3 (en) |
WO (1) | WO2002068174A1 (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2009065095A1 (en) * | 2007-11-16 | 2009-05-22 | Rasmus Norling | In-line system for de-salting fuel oil supplied to gas turbine engines |
US20100143523A1 (en) * | 2008-12-10 | 2010-06-10 | Chang Shou-Chih | Counter-rotating twin screw extruder |
US20100276340A1 (en) * | 2007-11-16 | 2010-11-04 | Rasmus Norling | In-line system for de-salting fuel oil supplied to gas turbine engines |
US20110001257A1 (en) * | 2009-07-01 | 2011-01-06 | Corey James Kenneally | Single screw extruder for dryer bar manufacture |
US20110000068A1 (en) * | 2009-07-01 | 2011-01-06 | Corey James Kenneally | Dryer bar having void volumes |
US20110199856A1 (en) * | 2008-10-21 | 2011-08-18 | Wook Ryol Hwang | Agitating vessel using baffles and agitator having improved agitating capability and including the same |
US20170106579A1 (en) * | 2015-10-19 | 2017-04-20 | Sumitomo Rubber Industries, Ltd. | Extruder |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102007047726A1 (en) * | 2007-10-05 | 2009-04-09 | Rieter Automatik Gmbh | Extrusion device for extruding molten synthetic material, has heating insert comprising elongated base, where external dimensions of base is formed in such manner that base is inserted into opening in starting valve in form-fit manner |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1184016A (en) * | 1915-11-12 | 1916-05-23 | Rubber Regenerating Co | Apparatus for treating plastic materials. |
US3480997A (en) | 1966-08-22 | 1969-12-02 | Heinz List | Apparatus for the thermal treatment of plastic materials |
US3482822A (en) * | 1968-01-30 | 1969-12-09 | Eugene J Krizak | Mixing device |
US3675902A (en) * | 1970-07-27 | 1972-07-11 | Union Carbide Corp | Mixing of fluid materials |
US5324108A (en) | 1990-04-02 | 1994-06-28 | Kleinewefers Kunststoffanlagen Gmbh | Arrangement for pin cylinder extruders |
US5480227A (en) | 1992-12-28 | 1996-01-02 | Krupp Maschinentechnik Gmbh | Screw extruder with shear-controlling diagonally extending pins |
JPH1177667A (en) | 1997-09-10 | 1999-03-23 | Bridgestone Cycle Co | Pin extruder |
-
2001
- 2001-02-14 EP EP01830096A patent/EP1232847A1/en not_active Withdrawn
-
2002
- 2002-02-11 US US10/399,111 patent/US6814481B2/en not_active Expired - Lifetime
- 2002-02-11 AT AT02711859T patent/ATE296722T1/en not_active IP Right Cessation
- 2002-02-11 WO PCT/EP2002/001417 patent/WO2002068174A1/en not_active Application Discontinuation
- 2002-02-11 EP EP02711859A patent/EP1360060B1/en not_active Expired - Lifetime
- 2002-02-11 ES ES02711859T patent/ES2242847T3/en not_active Expired - Lifetime
- 2002-02-11 DE DE60204425T patent/DE60204425T2/en not_active Expired - Lifetime
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1184016A (en) * | 1915-11-12 | 1916-05-23 | Rubber Regenerating Co | Apparatus for treating plastic materials. |
US3480997A (en) | 1966-08-22 | 1969-12-02 | Heinz List | Apparatus for the thermal treatment of plastic materials |
US3482822A (en) * | 1968-01-30 | 1969-12-09 | Eugene J Krizak | Mixing device |
US3675902A (en) * | 1970-07-27 | 1972-07-11 | Union Carbide Corp | Mixing of fluid materials |
US5324108A (en) | 1990-04-02 | 1994-06-28 | Kleinewefers Kunststoffanlagen Gmbh | Arrangement for pin cylinder extruders |
US5480227A (en) | 1992-12-28 | 1996-01-02 | Krupp Maschinentechnik Gmbh | Screw extruder with shear-controlling diagonally extending pins |
JPH1177667A (en) | 1997-09-10 | 1999-03-23 | Bridgestone Cycle Co | Pin extruder |
Non-Patent Citations (1)
Title |
---|
Patent Abstracts of Japan, vol. 1999, No. 08, Jun. 30, 1999 & JP 11 077667 A (Bridgestone Cycle Co), Mar. 23, 1999 abstract. |
Cited By (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20100276340A1 (en) * | 2007-11-16 | 2010-11-04 | Rasmus Norling | In-line system for de-salting fuel oil supplied to gas turbine engines |
US9540571B2 (en) | 2007-11-16 | 2017-01-10 | Triton Emission Solutions Inc. | In-line system for de-salting diesel oil supplied to gas turbine engines |
WO2009065095A1 (en) * | 2007-11-16 | 2009-05-22 | Rasmus Norling | In-line system for de-salting fuel oil supplied to gas turbine engines |
US20110199856A1 (en) * | 2008-10-21 | 2011-08-18 | Wook Ryol Hwang | Agitating vessel using baffles and agitator having improved agitating capability and including the same |
US9205389B2 (en) * | 2008-10-21 | 2015-12-08 | Industry-Academic Cooperation Foundation Gyeongsang National University | Agitating vessel using baffles and agitator having improved agitating capability and including the same |
US20100143523A1 (en) * | 2008-12-10 | 2010-06-10 | Chang Shou-Chih | Counter-rotating twin screw extruder |
US8596856B2 (en) * | 2008-12-10 | 2013-12-03 | Shuo-Chih Chang | Counter-rotating twin screw extruder |
WO2011002743A1 (en) | 2009-07-01 | 2011-01-06 | The Procter & Gamble Company | Dryer bar having void volumes |
US8338359B2 (en) | 2009-07-01 | 2012-12-25 | The Procter & Gamble Company | Dryer bar having void volumes |
US8440124B2 (en) | 2009-07-01 | 2013-05-14 | The Procter & Gamble Company | Single screw extruder for dryer bar manufacture |
US20110000068A1 (en) * | 2009-07-01 | 2011-01-06 | Corey James Kenneally | Dryer bar having void volumes |
WO2011002742A1 (en) | 2009-07-01 | 2011-01-06 | The Procter & Gamble Company | Single screw extruder for dryer bar manufacture |
US20110001257A1 (en) * | 2009-07-01 | 2011-01-06 | Corey James Kenneally | Single screw extruder for dryer bar manufacture |
US20170106579A1 (en) * | 2015-10-19 | 2017-04-20 | Sumitomo Rubber Industries, Ltd. | Extruder |
US11104053B2 (en) * | 2015-10-19 | 2021-08-31 | Sumitomo Rubber Industries, Ltd. | Extruder |
Also Published As
Publication number | Publication date |
---|---|
DE60204425T2 (en) | 2006-03-23 |
DE60204425D1 (en) | 2005-07-07 |
EP1360060B1 (en) | 2005-06-01 |
EP1232847A1 (en) | 2002-08-21 |
US20040115297A1 (en) | 2004-06-17 |
EP1360060A1 (en) | 2003-11-12 |
ES2242847T3 (en) | 2005-11-16 |
ATE296722T1 (en) | 2005-06-15 |
WO2002068174A1 (en) | 2002-09-06 |
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Legal Events
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